US4909037A - Control system for once-through boilers - Google Patents
Control system for once-through boilers Download PDFInfo
- Publication number
- US4909037A US4909037A US07/401,276 US40127689A US4909037A US 4909037 A US4909037 A US 4909037A US 40127689 A US40127689 A US 40127689A US 4909037 A US4909037 A US 4909037A
- Authority
- US
- United States
- Prior art keywords
- boiler
- signal
- rate
- indicative
- producing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000000446 fuel Substances 0.000 claims abstract description 65
- 230000008859 change Effects 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 13
- 230000004044 response Effects 0.000 claims description 12
- 230000009471 action Effects 0.000 claims description 3
- 239000003245 coal Substances 0.000 abstract description 6
- 238000005259 measurement Methods 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 5
- 238000010304 firing Methods 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 238000009530 blood pressure measurement Methods 0.000 description 1
- 230000000368 destabilizing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B35/00—Control systems for steam boilers
- F22B35/06—Control systems for steam boilers for steam boilers of forced-flow type
- F22B35/10—Control systems for steam boilers for steam boilers of forced-flow type of once-through type
Definitions
- This invention relates to a control system for controlling boiler inputs in a once-through boiler so as to maintain the throttle pressure of the boiler at a desired value while maintaining the required steam flow to a load, such as a turbine-generator.
- mill storage capacity In addition to the problem of changing heating values in coal delivery systems, these systems present other problems in that the fuel rate measurement typically doesn't reflect the actual coal flow to the furnace due to two main considerations: mill storage capacity and mill response capability. Mill coal flow is typically controlled by adjusting feeder speed, using a tachometer output to measure feeder speed and hence fuel input. All mills have significant capacity so that fuel flow into the mill does not necessarily represent the actual fuel flow going to the furnace of the boiler, let alone the BTU input to the boiler. Typical time constants for a mill may be in the range of 100 to 160 seconds before a change of mill input will be seen as a significant output to the furnace. These fuel delivery system dynamics may advantageously be taken care of with a "Mill Model" using feeder speed as its input. This model would typically have a dead time and a first order lag.
- the method involves comparing a demand signal indicative of the desired energy output rate for the boiler with a signal indicative of the heat released to the furnace of the boiler and controlling fuel input rate with a proportional and integral controller so that the fuel feed rate is controlled to bring the signals into equality, just as was done in the referenced patent.
- the heat release signal for this invention is different in that it is obtained by first calculating a lagged value of a quantity which corresponds to boiler output, such as steam flow or turbine first stage pressure, divided by fuel feed rate, as modeled by the fuel delivery system model including feeder speed and other fuel signals as applicable. That lagged value is then multiplied by the value of the fuel feed rate to obtain a signal equal to the steady state energy delivered to the furnace.
- FIG. 1 shows a circuit diagram of an analog execution of the form of the invention, which corresponds to the showing of FIG. 1 of the referenced patent except for the showing of the boiler without a drum so as to represent a once-through boiler and the showing for that part of the circuit which generates the signal on line 33, whose elements are shown with reference characters exceeding the number 119.
- the heat release signal on line 33 is compared to the demand signal on line 30 to produce an error signal on line 31, and the fuel feed is controlled by controller 12 from that error signal so as to maintain the error signal at zero.
- the controller operates in a like manner to keep the error signal at zero in order to maintain the BTU input to the boiler equal to the rate of energy output of the boiler while maintaining the throttle pressure at its set point.
- the heat release signal was made up of the sum of a signal P 1 , the turbine first stage pressure measurement, representing boiler output under steady state conditions, and a signal dP/dt representing the rate of change of the drum pressure and hence the rate at which stored energy is changing in the boiler.
- the compensation is done by the present system without destabilizing the fuel feed control system, which includes both proportional and integral or reset control, by introducing the compensation gradually through the use of a first order lag circuit 124.
- the rate at which the compensation is introduced should be a rate less than 1/10th the integration rate of the fuel controller 12.
- the output of the divider 122 is used as an input to the lag circuit 124 and the output of that lag circuit is then one of the inputs to the multiplier 126, the other input being the signal Q FI which is obtained from the output of the mill model 128.
- the mill model 128 functions to characterize the fuel feed signal in accordance with the dynamic characteristics of the mill 14.
- the feeder speed which is measured by connecting a tachometer 130 to the shaft of the feeder drive motor 70, is used as an input to the mill model which through the introduction of a dead time and a first order lag, for example, will characterize the feeder rate as represented by the signal from the tachometer to produce a fuel feed signal which closely matches the actual fuel feed provided at the output of the mill 14 to the furnace of the boiler.
- Q FI the output of the mill model, will closely match the actual fuel feed rate.
- the boiler output signal Q BO is obtained by measuring the first stage pressure P 1 in the turbine 48.
- the boiler output could also be measured by measuring the steam flow, or by measuring the output of the generator 46.
- a load change such as would be signified by a change in the position of the throttle valve 22 to provide a change in the output of the generator 46 would cause a comparable change in the demand signal on line 30.
- the controller would change the fuel input by changing the speed of motor 70 so as to maintain the signal on line 33 equal to that on line 30.
- the output of the divider would respond to the change in P 1 , but the output of the lag circuit 124 would not have changed thus leaving the value of the signal on line 33 unchanged except for the changes which occur in response to the control action of controller 12. Since the control action is faster than the lag circuit, the fuel feed will be controlled to meet the new load with a minimum of interaction from the network 120.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Abstract
Description
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/401,276 US4909037A (en) | 1989-08-31 | 1989-08-31 | Control system for once-through boilers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/401,276 US4909037A (en) | 1989-08-31 | 1989-08-31 | Control system for once-through boilers |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4909037A true US4909037A (en) | 1990-03-20 |
Family
ID=23587085
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/401,276 Expired - Lifetime US4909037A (en) | 1989-08-31 | 1989-08-31 | Control system for once-through boilers |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US4909037A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2276225A (en) * | 1993-03-12 | 1994-09-21 | Westinghouse Electric Corp | Temperature control of boiler steam |
| WO2003102472A1 (en) * | 2002-06-03 | 2003-12-11 | Metso Automation Oy | Method and apparatus in connection with a power boiler |
| US6712012B1 (en) * | 1999-10-04 | 2004-03-30 | Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno | Control system for an incineration plant, such as for instance a refuse incineration plant |
| US20060070361A1 (en) * | 2004-10-05 | 2006-04-06 | Caterpillar Inc. | Filter service system and method |
| US20060070359A1 (en) * | 2004-10-05 | 2006-04-06 | Caterpillar Inc. | Filter service system |
| US20060144223A1 (en) * | 2004-10-05 | 2006-07-06 | Sellers Cheryl L | Deposition system and method |
| US20060156919A1 (en) * | 2004-10-05 | 2006-07-20 | Sellers Cheryl L | Filter service system and method |
| US20160032784A1 (en) * | 2014-07-29 | 2016-02-04 | Alstom Technology Ltd | Method for low load operation of a power plant with a once-through boiler |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3545207A (en) * | 1969-07-23 | 1970-12-08 | Leeds & Northrup Co | Boiler control system |
| US3802189A (en) * | 1972-01-13 | 1974-04-09 | Leeds & Northrup Co | Boiler-turbine control system |
| US3896623A (en) * | 1974-03-06 | 1975-07-29 | Leeds & Northrup Co | Boiler-turbine control system |
| US4174618A (en) * | 1978-04-03 | 1979-11-20 | Leeds & Northrup Company | Decoupled cascade control system |
| US4213304A (en) * | 1978-11-24 | 1980-07-22 | Leeds & Northrup Company | Boiler control system |
-
1989
- 1989-08-31 US US07/401,276 patent/US4909037A/en not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3545207A (en) * | 1969-07-23 | 1970-12-08 | Leeds & Northrup Co | Boiler control system |
| US3802189A (en) * | 1972-01-13 | 1974-04-09 | Leeds & Northrup Co | Boiler-turbine control system |
| US3896623A (en) * | 1974-03-06 | 1975-07-29 | Leeds & Northrup Co | Boiler-turbine control system |
| US4174618A (en) * | 1978-04-03 | 1979-11-20 | Leeds & Northrup Company | Decoupled cascade control system |
| US4213304A (en) * | 1978-11-24 | 1980-07-22 | Leeds & Northrup Company | Boiler control system |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2276225A (en) * | 1993-03-12 | 1994-09-21 | Westinghouse Electric Corp | Temperature control of boiler steam |
| US6712012B1 (en) * | 1999-10-04 | 2004-03-30 | Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno | Control system for an incineration plant, such as for instance a refuse incineration plant |
| WO2003102472A1 (en) * | 2002-06-03 | 2003-12-11 | Metso Automation Oy | Method and apparatus in connection with a power boiler |
| US7410529B2 (en) | 2004-10-05 | 2008-08-12 | Caterpillar Inc. | Filter service system and method |
| US20060070359A1 (en) * | 2004-10-05 | 2006-04-06 | Caterpillar Inc. | Filter service system |
| US20060144223A1 (en) * | 2004-10-05 | 2006-07-06 | Sellers Cheryl L | Deposition system and method |
| US20060156919A1 (en) * | 2004-10-05 | 2006-07-20 | Sellers Cheryl L | Filter service system and method |
| US7384455B2 (en) | 2004-10-05 | 2008-06-10 | Caterpillar Inc. | Filter service system and method |
| US20060070361A1 (en) * | 2004-10-05 | 2006-04-06 | Caterpillar Inc. | Filter service system and method |
| US7419532B2 (en) * | 2004-10-05 | 2008-09-02 | Caterpillar Inc. | Deposition system and method |
| US7462222B2 (en) | 2004-10-05 | 2008-12-09 | Caterpillar Inc. | Filter service system |
| US20090000471A1 (en) * | 2004-10-05 | 2009-01-01 | Caterpillar Inc. | Filter service system and method |
| US8252093B2 (en) | 2004-10-05 | 2012-08-28 | Cheryl Lynn Sellers | Filter service system and method |
| US8608834B2 (en) | 2004-10-05 | 2013-12-17 | Caterpillar Inc. | Filter service system and method |
| US20160032784A1 (en) * | 2014-07-29 | 2016-02-04 | Alstom Technology Ltd | Method for low load operation of a power plant with a once-through boiler |
| US10196939B2 (en) * | 2014-07-29 | 2019-02-05 | General Electric Technology Gmbh | Method for low load operation of a power plant with a once-through boiler |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: GENERAL SIGNAL CORPORATION A CORP. OF NY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:HUBBY, ROBERT N.;REEL/FRAME:005118/0768 Effective date: 19890821 |
|
| STCF | Information on status: patent grant |
Free format text: PATENTED CASE |
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| FEPP | Fee payment procedure |
Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
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| FPAY | Fee payment |
Year of fee payment: 4 |
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| AS | Assignment |
Owner name: INDUSTRIAL CONTROL SERVICES TECHNOLOGY LIMITED, EN Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:GENERAL SIGNAL CORPORATION;REEL/FRAME:007417/0338 Effective date: 19950309 |
|
| AS | Assignment |
Owner name: INDUSTRIAL CONTROL SERVICES TECHNOLOGY LIMITED, UN Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:LEEDS & NORTHRUP CO.;REEL/FRAME:008162/0928 Effective date: 19950309 |
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| FPAY | Fee payment |
Year of fee payment: 8 |
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| AS | Assignment |
Owner name: MAX CONTROL SYSTEMS INC., PENNSYLVANIA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:INDUSTRIAL CONTROL SERVICES TECHNOLOGY LIMITED;REEL/FRAME:011044/0857 Effective date: 20000605 |
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| FEPP | Fee payment procedure |
Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
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| FPAY | Fee payment |
Year of fee payment: 12 |